US3445244A - Solid vinegar - Google Patents
Solid vinegar Download PDFInfo
- Publication number
- US3445244A US3445244A US527729A US3445244DA US3445244A US 3445244 A US3445244 A US 3445244A US 527729 A US527729 A US 527729A US 3445244D A US3445244D A US 3445244DA US 3445244 A US3445244 A US 3445244A
- Authority
- US
- United States
- Prior art keywords
- vinegar
- dextrin
- solids
- spray dried
- gum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 235000021419 vinegar Nutrition 0.000 title description 37
- 239000000052 vinegar Substances 0.000 title description 37
- 239000007787 solid Substances 0.000 title description 17
- 239000004375 Dextrin Substances 0.000 description 17
- 229920001353 Dextrin Polymers 0.000 description 17
- 235000019425 dextrin Nutrition 0.000 description 17
- 239000007921 spray Substances 0.000 description 14
- 244000215068 Acacia senegal Species 0.000 description 11
- 229920000084 Gum arabic Polymers 0.000 description 11
- 235000010489 acacia gum Nutrition 0.000 description 11
- 235000006491 Acacia senegal Nutrition 0.000 description 8
- 108010010803 Gelatin Proteins 0.000 description 8
- 229920000159 gelatin Polymers 0.000 description 8
- 239000008273 gelatin Substances 0.000 description 8
- 235000019322 gelatine Nutrition 0.000 description 8
- 235000011852 gelatine desserts Nutrition 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 235000013339 cereals Nutrition 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000003925 fat Substances 0.000 description 5
- 235000019197 fats Nutrition 0.000 description 5
- 150000001720 carbohydrates Chemical class 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- 108010068370 Glutens Proteins 0.000 description 3
- 239000000205 acacia gum Substances 0.000 description 3
- 235000021312 gluten Nutrition 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 125000005456 glyceride group Chemical group 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 235000018102 proteins Nutrition 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- IWYGVDBZCSCJGT-UHFFFAOYSA-N 1-(2,5-dimethoxy-4-methylphenyl)-n-methylpropan-2-amine Chemical compound CNC(C)CC1=CC(OC)=C(C)C=C1OC IWYGVDBZCSCJGT-UHFFFAOYSA-N 0.000 description 1
- 241000416162 Astragalus gummifer Species 0.000 description 1
- 244000060011 Cocos nucifera Species 0.000 description 1
- 235000013162 Cocos nucifera Nutrition 0.000 description 1
- 235000019483 Peanut oil Nutrition 0.000 description 1
- 229920001615 Tragacanth Polymers 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 244000098338 Triticum aestivum Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000011260 aqueous acid Substances 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 229940095714 cider vinegar Drugs 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000015142 cultured sour cream Nutrition 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000010514 hydrogenated cottonseed oil Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000312 peanut oil Substances 0.000 description 1
- 235000014438 salad dressings Nutrition 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12J—VINEGAR; PREPARATION OR PURIFICATION THEREOF
- C12J1/00—Vinegar; Preparation or purification thereof
Definitions
- the present invention relates to spray drying vinegar.
- Another object is to entrap the characteristic vinegar flavor in a dry powder.
- the preferred enrobing agent is gum arabic.
- dextrin as a coating or en-robing agent.
- carbohydrate gums such as gum tragacanth.
- fats and/or emulsifiers e.g. mono and di glycerides to (1) absorb fat soluble flavors, (2) prevent dusting of the final powder and (3) to cut down foaming during processing.
- Suitable fats include vegetable fats such as cocoanut oil, hydrogenated castor oil, hydrogenated cottonseed oil, corn oil, safllower oil, peanut oil.
- the vinegar can be from 60 grain to 500 grain, with 200-400 grain vinegar (i.e. 20-40%) being preferred. It is not economically feasible to use vinegar below 60 grain because of the large amount of water which must be removed.
- the spray dried vinegar products of the present invention can be used to impart vinegar flavor in dry form for salad dressings, sour cream, spaghetti sauce, dry mix preparations, etc.
- the aqueous mixture which is spray dried has 25-60% solids (i.e. nonvvater) content. It is preferred to use as high a solids concentration as is possible so as to keep the drying rate at a maximum and the resultant powder at the lowest temperature.
- the solids content prior to drying should be such as to give a fluid, homogenous emulsion.
- Percent Vinegar 5 to 60 Gum acacia 25 to 95 United States Patent 0 Fee
- dextrin When dextrin is employed it is used in an amount of 30 to of total solids.
- Gelatin when employed, is used in an amount of 2 to 20%.
- Fats when employed, are used in an amount of 0.1 to 10%.
- Mono and di glycerides are used in the same amount as the fats.
- the aqueous mixture of gum or dextrin is normally pasteurized, e.g. at 140-165 F.
- the vinegar is not added to the hot gum or dextrin solution or volatile materials will be lost.
- the temperature therefore is preferably lowered to not over 125 F., most preferably at IOU- F. prior to addition of the vinegar.
- the emulsion should be well homogenized to entrap the vinegar flavor. Homogenization pressures are usually in the range of 1000-5000 p.s.i.
- Example 1 Parts White vinegar solids 20 Gum acacia 80
- the method of preparation was as follows: Gum acacia was dissolved in enough warm water to give a 35% total aqueous solids suspension after addition of the vinegar. (The term solids as used in the present specification when applied to vinegar includes all the nonaqueous portion of the vinegar.)
- the gum acacia solution was pasteurized at 160 F. for 30 minutes, cooled to F. and concentrated (300 grain) white vinegar added. The batch was stirred until uniform, homogenized at 2000 psi. and spray dried in a horizontal concurrent flow spray dryer at 350 F.
- a similar spray dried product was obtained by replacing the white vinegar by cider vinegar.
- Example 2 Parts White vinegar solids 50 Gum acacia solids 50 The process of Example 1 was repeated to produce a spray dried vinegar enrobed in the gum acacia.
- Example 3 Parts White vinegar solids 20 Gum acacia '65 Gelatin type A 15 The process of Example 1 was repeated to produce a spray dried vinegar product.
- Example 4 Parts White vinegar solids 20 Globe yellow dextrin 80 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
- Example 5 Parts White vinegar solids 50 Globe yellow dextrin 50 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
- Example 6 Parts White vinegar solids 20 Globe yellow dextrin 65 Gelatin, type A 15 The procedure of Example 1 was repeated to obtain 3 spray dried vinegar enrobed in a mixture of dextrin and gelat'm.
- a composition comprising to 60% spray dried vinegar enrobed in a spray dried member of the group consisting of 25 to 95% carbohydrate gums and 30 to 95% dextrin.
- a product according to claim 1 including 2 to of a member of the group consisting of gelatin and gluten.
- a product according to claim 1 containing 5 to 60% vinegar and to 95 gum acacia.
- a product according to claim 3 including 2 to 20% of gelatin.
- a product according to claim 1 containing 5 to 60% vinegar and to 95% dextrin.
- a product according to claim 5 including 2 to 20% gelatin.
- a process of preparing the product of claim 1 comprising passing an aqueous mixture containing 25 to solids of vinegar and an enrobing agent of the group consisting of carbohydrate gums and dextrin wherein the solids comprise 5-60% vinegar and 25-95% of the References Cited UNITED STATES PATENTS 4/1931 Bornegg 99-206 9/ 1960 Sanna -9956 FOREIGN PATENTS 23,064 10/ 1963 Japan.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Seasonings (AREA)
- Jellies, Jams, And Syrups (AREA)
Description
3,445,244 SOLID VINEGAR Peter Paul Noznick, Evanston, and Charles W. Tatter, Homewood, Ill., assignors to Beatrice Foods Co., Chicago, 11]., a corporation of Delaware No Drawing. Filed Feb. 16, 1966, Ser. No. 527,729
Int. Cl. C12j 1/00 US. Cl. 99-147 9 Claims ABSTRACT OF THE DISCLOSURE Aqueous vinegar is spray dried with a carbohydrate gum or dextrin as an enrobing agent. Gelatin or gluten can also be present.
The present invention relates to spray drying vinegar.
It is an object of the present invention to form spray dried vinegar.
Another object is to entrap the characteristic vinegar flavor in a dry powder.
Still further objects and the entire scope of applicability of the present invention will become apparent from the detailed description given hereinafter; it should be understood, however, that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
It has now been found that these objects can be attained by spray drying vinegar in the presence of an enrobing agent.
The preferred enrobing agent is gum arabic. In place of all or part of the gum arabic there can be used dextrin as a coating or en-robing agent. Also, there can be used other carbohydrate gums such as gum tragacanth.
There can also be used certain proteins in conjunction with the gum arabic and/or dextrin. Thus, there can be employed A type gelatin and gluten (the acid soluble protein from wheat).
Optionally, there can be added fats and/or emulsifiers, e.g. mono and di glycerides to (1) absorb fat soluble flavors, (2) prevent dusting of the final powder and (3) to cut down foaming during processing. Suitable fats include vegetable fats such as cocoanut oil, hydrogenated castor oil, hydrogenated cottonseed oil, corn oil, safllower oil, peanut oil.
The vinegar can be from 60 grain to 500 grain, with 200-400 grain vinegar (i.e. 20-40%) being preferred. It is not economically feasible to use vinegar below 60 grain because of the large amount of water which must be removed.
The spray dried vinegar products of the present invention can be used to impart vinegar flavor in dry form for salad dressings, sour cream, spaghetti sauce, dry mix preparations, etc.
Unless otherwise indicated, all parts and percentages are by weight.
Usually the aqueous mixture which is spray dried has 25-60% solids (i.e. nonvvater) content. It is preferred to use as high a solids concentration as is possible so as to keep the drying rate at a maximum and the resultant powder at the lowest temperature. The solids content prior to drying should be such as to give a fluid, homogenous emulsion.
The range of proportions of materials which can be employed are as follows:
Percent Vinegar (nonaqueous basis) 5 to 60 Gum acacia 25 to 95 United States Patent 0 Fee When dextrin is employed it is used in an amount of 30 to of total solids. Gelatin, when employed, is used in an amount of 2 to 20%. Fats, when employed, are used in an amount of 0.1 to 10%. Mono and di glycerides are used in the same amount as the fats.
The aqueous mixture of gum or dextrin is normally pasteurized, e.g. at 140-165 F.
Preferably, the vinegar is not added to the hot gum or dextrin solution or volatile materials will be lost. The temperature therefore is preferably lowered to not over 125 F., most preferably at IOU- F. prior to addition of the vinegar. The emulsion should be well homogenized to entrap the vinegar flavor. Homogenization pressures are usually in the range of 1000-5000 p.s.i.
When employing dextrin it is important to keep the contact time between the aqueous acid and dextrin at a minimum to prevent hydrolysis.
Example 1 Parts White vinegar solids 20 Gum acacia 80 In the above example the method of preparation was as follows: Gum acacia was dissolved in enough warm water to give a 35% total aqueous solids suspension after addition of the vinegar. (The term solids as used in the present specification when applied to vinegar includes all the nonaqueous portion of the vinegar.) The gum acacia solution was pasteurized at 160 F. for 30 minutes, cooled to F. and concentrated (300 grain) white vinegar added. The batch was stirred until uniform, homogenized at 2000 psi. and spray dried in a horizontal concurrent flow spray dryer at 350 F.
A similar spray dried product was obtained by replacing the white vinegar by cider vinegar.
Example 2 Parts White vinegar solids 50 Gum acacia solids 50 The process of Example 1 was repeated to produce a spray dried vinegar enrobed in the gum acacia.
Example 3 Parts White vinegar solids 20 Gum acacia '65 Gelatin type A 15 The process of Example 1 was repeated to produce a spray dried vinegar product.
Example 4 Parts White vinegar solids 20 Globe yellow dextrin 80 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
Example 5 Parts White vinegar solids 50 Globe yellow dextrin 50 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
Example 6 Parts White vinegar solids 20 Globe yellow dextrin 65 Gelatin, type A 15 The procedure of Example 1 was repeated to obtain 3 spray dried vinegar enrobed in a mixture of dextrin and gelat'm.
We claim:
1. A composition comprising to 60% spray dried vinegar enrobed in a spray dried member of the group consisting of 25 to 95% carbohydrate gums and 30 to 95% dextrin.
2. A product according to claim 1 including 2 to of a member of the group consisting of gelatin and gluten.
3. A product according to claim 1 containing 5 to 60% vinegar and to 95 gum acacia.
4. A product according to claim 3 including 2 to 20% of gelatin.
5. A product according to claim 1 containing 5 to 60% vinegar and to 95% dextrin.
6. A product according to claim 5 including 2 to 20% gelatin.
7. A process of preparing the product of claim 1 comprising passing an aqueous mixture containing 25 to solids of vinegar and an enrobing agent of the group consisting of carbohydrate gums and dextrin wherein the solids comprise 5-60% vinegar and 25-95% of the References Cited UNITED STATES PATENTS 4/1931 Bornegg 99-206 9/ 1960 Sanna -9956 FOREIGN PATENTS 23,064 10/ 1963 Japan.
RAYMOND N. JONES, Primary Examiner.
R. B. ANDEWELT, Assistant Examiner.
US. Cl. X.R. 99-199
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US52772966A | 1966-02-16 | 1966-02-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3445244A true US3445244A (en) | 1969-05-20 |
Family
ID=24102691
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US527729A Expired - Lifetime US3445244A (en) | 1966-02-16 | 1966-02-16 | Solid vinegar |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3445244A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3630756A (en) * | 1970-03-18 | 1971-12-28 | Ross Alexander Smith | Vinegar-type flavor composition |
| US3898344A (en) * | 1973-05-24 | 1975-08-05 | Us Army | Packaged dry imitation vinegar product |
| US4713251A (en) * | 1985-12-18 | 1987-12-15 | Durkee Industrial Foods Corp. | Process for encapsulating liquid acids and product |
| FR2755610A1 (en) * | 1996-11-14 | 1998-05-15 | Dukan Pierre | Preparation of dry extract from vinegar that has been enriched with sludge from filtration of crude vinegar |
| US20120201950A1 (en) * | 2005-09-15 | 2012-08-09 | Triad Resource Technologies, Llc | Compositions for improving flavor and safety of marinated meat products |
| US20120208740A1 (en) * | 2011-02-14 | 2012-08-16 | Chemlink Laboratories, Llc | Method for preparing a solid form of acetic acid and products thereof |
| US20150225683A1 (en) * | 2012-08-01 | 2015-08-13 | Purac Biochem B.V. | Preparation of a powdered vinegar |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1800501A (en) * | 1924-03-11 | 1931-04-14 | Fruit Growers Exchange Ca | Method of drying fruit juices |
| US2953457A (en) * | 1957-06-24 | 1960-09-20 | Sanna Dairies Inc | Method for drying food materials |
-
1966
- 1966-02-16 US US527729A patent/US3445244A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1800501A (en) * | 1924-03-11 | 1931-04-14 | Fruit Growers Exchange Ca | Method of drying fruit juices |
| US2953457A (en) * | 1957-06-24 | 1960-09-20 | Sanna Dairies Inc | Method for drying food materials |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3630756A (en) * | 1970-03-18 | 1971-12-28 | Ross Alexander Smith | Vinegar-type flavor composition |
| US3898344A (en) * | 1973-05-24 | 1975-08-05 | Us Army | Packaged dry imitation vinegar product |
| US4713251A (en) * | 1985-12-18 | 1987-12-15 | Durkee Industrial Foods Corp. | Process for encapsulating liquid acids and product |
| FR2755610A1 (en) * | 1996-11-14 | 1998-05-15 | Dukan Pierre | Preparation of dry extract from vinegar that has been enriched with sludge from filtration of crude vinegar |
| US9578893B2 (en) | 2005-09-15 | 2017-02-28 | Triad Resource Technologies, Llc | Compositions for improving flavor and safety of marinated meat products |
| US8877280B2 (en) * | 2005-09-15 | 2014-11-04 | Triad Resource Technologies, Llc | Compositions for improving flavor and safety of marinated meat products |
| US20120201950A1 (en) * | 2005-09-15 | 2012-08-09 | Triad Resource Technologies, Llc | Compositions for improving flavor and safety of marinated meat products |
| US20120208740A1 (en) * | 2011-02-14 | 2012-08-16 | Chemlink Laboratories, Llc | Method for preparing a solid form of acetic acid and products thereof |
| US8859482B2 (en) * | 2011-02-14 | 2014-10-14 | Chemlink Laboratories, Llc | Method for preparing a solid form of acetic acid and products thereof |
| US9068146B2 (en) | 2011-02-14 | 2015-06-30 | Chemlink Laboratories, Llc | Solid form of acetic acid and products thereof |
| US20150225683A1 (en) * | 2012-08-01 | 2015-08-13 | Purac Biochem B.V. | Preparation of a powdered vinegar |
| EP2880146B1 (en) | 2012-08-01 | 2016-10-26 | Purac Biochem bv | Preparation of a powdered vinegar |
| EP3115448A1 (en) * | 2012-08-01 | 2017-01-11 | Purac Biochem B.V. | Preparation of a powdered vinegar |
| US10752871B2 (en) * | 2012-08-01 | 2020-08-25 | Purac Biochem B.V. | Preparation of a powdered vinegar |
| US11466238B2 (en) | 2012-08-01 | 2022-10-11 | Purac Biochem B.V. | Preparation of a powdered vinegar |
| US12252674B2 (en) | 2012-08-01 | 2025-03-18 | Purac Biochem B.V. | Preparation of a powdered vinegar |
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